CN1775849A - Method for preparing high-temperature-rusistance water-expansible rubber - Google Patents

Method for preparing high-temperature-rusistance water-expansible rubber Download PDF

Info

Publication number
CN1775849A
CN1775849A CN 200510019972 CN200510019972A CN1775849A CN 1775849 A CN1775849 A CN 1775849A CN 200510019972 CN200510019972 CN 200510019972 CN 200510019972 A CN200510019972 A CN 200510019972A CN 1775849 A CN1775849 A CN 1775849A
Authority
CN
China
Prior art keywords
water
rubber
temperature
rusistance
expansible
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN 200510019972
Other languages
Chinese (zh)
Other versions
CN1331936C (en
Inventor
刘长生
周爱军
丁军平
周浪
汪艳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wuhan Chemistry College
Original Assignee
Wuhan Chemistry College
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wuhan Chemistry College filed Critical Wuhan Chemistry College
Priority to CNB2005100199726A priority Critical patent/CN1331936C/en
Publication of CN1775849A publication Critical patent/CN1775849A/en
Application granted granted Critical
Publication of CN1331936C publication Critical patent/CN1331936C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention relates to a method to manufacture functional rubber that could be expand when meet water between the temperature 25 degree centigrade and 150 degree centigrade. The process is: taking copolymerization by acrylic acid, sodium acrylate, acrylamide, heat endurable modification monomer and cross linking agent to gain heat endurable water absorbing resin powder, then, mixing and vulcanizing the mixture of the powder and rubber to gain high temperature endurable water expanding rubber. It has simple technology and low cost.

Description

A kind of method for preparing high-temperature-rusistance water-expansible rubber
Technical field
The present invention relates to the sealing material field, particularly a kind of preparation method of high-temperature-rusistance water-expansible rubber.
Background technology
Hydro-expansive rubber (Water swelling Rubber is called for short WSR) is a kind of new-type functional material, and it is upward introduced wetting ability functional group or hydrophilic component at traditional elastic matrix (rubber) and makes.Its mechanism of action is: when contacting with water, water molecules can be by diffusion, physical action such as capillary and surface adsorption enters in the WSR, and then form extremely strong avidity with hydrophilic radical in the rubber, because hydroaropic substance constantly absorbs moisture, cause rubber generation deformation, when anti deformational force and permeable pressure head reach balance, WSR keeps relative stability, and reaches elasticity and with the effect of water sealing.Since coming out beginning of the eighties late 1970s, WSR is with the dual sealing characteristic of its unique resilient seal sealing and water-swelling sealing.More and more be subject to people's attention.
The water-expansible rubber of holding back with the blending method preparation only just has good water absorbing properties under lower temperature, when temperature during greater than 30 ℃, the water-intake rate of hydro-expansive rubber reduces along with the rising of temperature, when temperature during near 70 ℃, water-swelling hardly, thereby greatly reduce the rate of expansion of hydro-expansive rubber, cause hydro-expansive rubber under high-temperature condition, to expand hardly, do not reach the sealing effect, to such an extent as to be difficult to come into operation, if can carry out modification to water-absorbing resin, make it under hot conditions, have stable structure and high-hydroscopicity energy, thereby widen its use range, for example improve and at high temperature have the water-swellable performance with significant with its hydro-expansive rubber of making as main raw material.
Zhang Yuhong, He Peixin etc. have studied the elastomeric temperature effect of CPE/P (AA-AM) water-swelling, and when temperature during greater than 30 ℃, the water-intake rate of hydro-expansive rubber reduces along with the rising of temperature, when temperature during near 70 ℃, and water-swelling hardly.
Summary of the invention
The objective of the invention is deficiencies such as heat resistance difference at existing hydro-expansive rubber existence, utilize the special monomer of structure as comonomer, preparing high temperature resistant water-absorbing resin, is feedstock production all has the water-swellable performance from 25 ℃ to 150 ℃ high temperature rubber by the physical blending technology with high temperature resistant water-absorbing resin and rubber.The characteristics of this method are: 1. hydro-expansive rubber broad application temperature range, all can use in 25 ℃ to 150 ℃ the temperature range; 2. prepare water-absorbing resin by simple inverse suspension polymerization method, make it then and the rubber physical blending is compound can obtain, this method technology is simple, and equipment requirements is low; 3. can control the water-swelling multiplying power by the proportioning that changes water-absorbing resin and rubber, thereby expansion multiplying power is controlled.
The objective of the invention is to adopt following technical measures to realize:
With mass ratio is vinylformic acid, sodium acrylate, acrylamide, heat resist modification monomer and the linking agent of 20-40: 30-60: 10-50: 10-60: 0.1-10, add in the reactor with 30-100mL solvent and 0.1-5 gram dispersion agent, constantly stir the back of heating up and drip the initiator copolyreaction, filter, methanol wash dry granularity less than the water-absorbing resin powder of 5 μ m, then with water-absorbing resin powder and rubber carry out blend in the mill, add vulcanizing ingredient vulcanize in 25 ℃ to 150 ℃ scopes, all have the water-swellable function rubber.
Described heat resist modification monomer is a vinyl-acetic ester, butyl acrylate, Octyl acrylate, vinylformic acid lauryl alcohol ester, vinylformic acid stearyl alcohol ester, butyl methacrylate, Octyl methacrylate, methacrylic acid lauryl alcohol ester, methacrylic acid stearyl alcohol ester, 2-acrylamido-2-methyl propane sulfonic acid (AMPS), 3-acrylamido oxypropyl trimethyl ammonium chloride, methacryloyl amido oxypropyl trimethyl ammonium chloride, dimethyl diallyl ammonium chloride or 2-methylacryoyloxyethyl-dimethyl dodecyl bromination ammonium.
Described linking agent is ethylene glycol diacrylate, Diethylene Glycol double methacrylate, polyoxyethylene glycol double methacrylate, N, N '-methylene-bisacrylamide, tetramethylolmethane double methacrylate or Vinylstyrene.
Described solvent is toluene, dimethylbenzene or hexanaphthene.
Described dispersion agent is span-80, Si Ban-60, Si Ban-20, tween-80, Tween-60, tween 20, Sodium dodecylbenzene sulfonate.
Described rubber is natural rubber, chloroprene rubber, ethylene-propylene rubber(EPR), paracril, chlorinatedpolyethylene, urethanes, viton, silicon rubber, isoprene-isobutylene rubber or styrene-butadiene rubber(SBR).
Described initiator is Potassium Persulphate or ammonium persulphate.
The present invention has following advantage: the particle diameter of (1) high temperature resistant water-absorbing resin is less, less than 5 μ m; (2) hydro-expansive rubber broad application temperature range, 25 ℃ to 150 ℃ high temperature all can use; (3) prepare by simple inverse suspension polymerization method that water-absorbing material makes it then and the rubber physical blending is compound can obtain this material, technology is simple, and equipment requirements is low; (4) can control the water-swelling multiplying power by the proportioning that changes water-absorbing resin and rubber, thereby expansion multiplying power is controlled.
Adopt the hydro-expansive rubber of the present invention's preparation at high temperature to have good water-swellable performance (seeing the following form) than common hydro-expansive rubber.Accurately take by weighing a certain amount of high-temperature-rusistance water-expansible rubber and place the minitype high voltage still, add 5-20 deionized water doubly, sealing is warming up to 150 ℃ of insulations after 3 days with autoclave, reduces to room temperature rapidly, takes out sample, wipes the moisture on surface with filter paper, carries out weighing.
The weight water-intake rate S of hydro-expansive rubber WCalculate as follows:
S W ( % ) = W 1 - W 2 W 1 × 100 %
W in the formula 1, W 2Be respectively the weight of sample suction front and back.
Relevant water-swellable experimental result
Sample type (150 ℃, the treatment time: 3day) Water-swellable multiplying power/%
Common hydro-expansive rubber sample of the present invention 50 400
Embodiment
Embodiment 1
With 2 gram vinylformic acid, 4 gram sodium acrylates, 2 gram acrylamides, 2 gram 2-acrylamido-2-methyl propane sulfonic acids, 0.2 gram Diethylene Glycol double methacrylate, 50ml toluene and 1 gram span-80 add in the reactor, be warming up to 75 ℃ under constantly stirring, drip the initiator potassium persulfate copolyreaction after 3 hours, filter, the dry water-absorbing resin powder that gets of methanol wash is then with 100 parts of paracrils, 30 parts of water-absorbing resin powders, 5 parts of zinc oxide, 2 parts of sulphur, 1 part of anti-aging agent, 20 parts of carbon blacks, 2.5 parts of promotor are carried out blend in mill, vulcanize can water-swellable in 25 ℃ to 150 ℃ scopes rubber.Take by weighing these hydro-expansive rubber 8 grams and deionized water 80 grams, put into autoclave, sealing is warming up to 150 ℃ of insulations after 3 days with autoclave, reduces to room temperature rapidly, takes out sample, wipes the moisture on surface with filter paper, and weighing gets 42 grams.
Embodiment 2
With 2.5 gram vinylformic acid, 3 gram sodium acrylates, 3 gram acrylamides, 1.5 gram 3-acrylamido oxypropyl trimethyl ammonium chloride (APTAC), 0.1 gram N, N '-methylene-bisacrylamide, 50mL solvent hexanaphthene and 1 Ke Siban-60 add in the reactor, be warming up to 60 ℃ under constantly stirring, drip the initiator potassium persulfate copolyreaction after 4 hours, filter, the dry water-absorbing resin powder that gets of methanol wash is then with 100 parts of paracrils, 30 parts of water-absorbing resin powders, 5 parts of zinc oxide, 2 parts of sulphur, 1 part of anti-aging agent, 20 parts of carbon blacks, 2.5 parts of promotor are carried out blend in mill, vulcanize can water-swellable in 25 ℃ to 150 ℃ scopes rubber.Take by weighing these hydro-expansive rubber 8 grams and deionized water 80 grams, put into autoclave, sealing is warming up to 150 ℃ of insulations after 3 days with autoclave, reduces to room temperature rapidly, takes out sample, wipes the moisture on surface with filter paper, and weighing gets 43 grams.
Embodiment 3
With 3 gram vinylformic acid, 3.5 gram sodium acrylate, 1.5 gram acrylamide, 2 gram methacryloyl amido oxypropyl trimethyl ammonium chlorides (MPTMA), 0.3 gram N, N '-methylene-bisacrylamide, 50mL solvent hexanaphthene and 1 Ke Siban-60 add in the reactor, are warming up to 85 ℃ under constantly stirring, and drip the initiator ammonium persulfate copolyreaction after 4 hours, filter, the dry water-absorbing resin powder that gets of methanol wash, then with 100 parts of chloroprene rubbers, 30 parts of water-absorbing resin powders, 1 part of stearic acid, 5 parts of zinc oxide, 4 parts of magnesium oxide, 1 part of anti-aging agent, 30 parts of potter's clay carry out blend in mill, vulcanize to such an extent that in 25 ℃ to 150 ℃ scopes, can hold back water swellable rubber.Take by weighing these hydro-expansive rubber 8 grams and deionized water 80 grams, put into autoclave, sealing is warming up to 150 ℃ of insulations after 3 days with autoclave, reduces to room temperature rapidly, takes out sample, wipes the moisture on surface with filter paper, and weighing gets 39 grams.
Embodiment 4
With 3 gram vinylformic acid, 3 gram sodium acrylates, 3 gram acrylamides, 1 gram dimethyl diallyl ammonium chloride (DMDAAC), 0.2 gram Diethylene Glycol double methacrylate, 50mL solvent hexanaphthene and 1 Ke Siban-60 add in the reactor, be warming up to 75 ℃ under constantly stirring, drip the initiator ammonium persulfate copolyreaction after 4 hours, filter, the dry water-absorbing resin powder that gets of methanol wash, then with 100 parts of natural rubbers, 30 parts of water-absorbing resin powders, 2.5 parts of sulphur, 1 part of promotor, 5 parts of zinc oxide, 2.5 part stearic acid, 20 parts of carbon blacks, 1 part of anti-aging agent carries out blend in mill, vulcanize can water-swellable in 25 ℃ to 150 ℃ scopes rubber.Take by weighing these hydro-expansive rubber 8 grams and deionized water 80 grams, put into autoclave, sealing is warming up to 150 ℃ of insulations after 3 days with autoclave, reduces to room temperature rapidly, takes out sample, wipes the moisture on surface with filter paper, and weighing gets 41 grams.
Embodiment 5
With 2.5 gram vinylformic acid, 3 gram sodium acrylates, 3.5 gram acrylamide, 1 gram dimethyl diallyl ammonium chloride (DMDAAC), 0.4 Diethylene Glycol double methacrylate, 50mL solvent hexanaphthene and 1 Ke Siban-60 add in the reactor, be warming up to 75 ℃ under constantly stirring, drip the initiator ammonium persulfate copolyreaction after 4 hours, filter, the dry water-absorbing resin powder that gets of methanol wash is then with 100 parts of ethylene-propylene rubber(EPR), 30 parts of water-absorbing resin powders, 5 parts of zinc oxide, 1 part of stearic acid, 2 parts of promotor, 1.5 part sulphur, 20 parts of carbon blacks carry out blend in mill, vulcanize can water-swellable in 25 ℃ to 150 ℃ scopes rubber.Take by weighing these hydro-expansive rubber 8 grams and deionized water 80 grams, put into autoclave, sealing is warming up to 150 ℃ of insulations after 3 days with autoclave, reduces to room temperature rapidly, takes out sample, wipes the moisture on surface with filter paper, and weighing gets 43 grams.
Embodiment 6
With 2 gram vinylformic acid, 3 gram sodium acrylates, 3 gram acrylamides, 2 gram 2-methylacryoyloxyethyl-dimethyl dodecyl bromination ammoniums (DMDA), 0.4 gram tetramethylolmethane double methacrylate, 50mL solvent hexanaphthene and 1 Ke Siban-60 add in the reactor, be warming up to 75 ℃ under constantly stirring, drip the copolyreaction of initiator ammonium peroxydisulfate after 4 hours, filter, the dry water-absorbing resin powder that gets of methanol wash is then with 100 parts of ethylene-propylene rubber(EPR), 30 parts of water-absorbing resin powders, 5 parts of zinc oxide, 1 part of stearic acid, 2 parts of promotor, 1.5 part sulphur, 20 parts of carbon blacks carry out blend in mill, vulcanize can water-swellable in 25 ℃ to 150 ℃ scopes rubber.Take by weighing these hydro-expansive rubber 8 grams and deionized water 80 grams, put into autoclave, sealing is warming up to 150 ℃ of insulations after 3 days with autoclave, reduces to room temperature rapidly, takes out sample, wipes the moisture on surface with filter paper, and weighing gets 41 grams.
Embodiment 7
With 2.5 gram vinylformic acid, 3 gram sodium acrylates, 2 gram acrylamides, 2.5 gram 2-methylacryoyloxyethyl-dimethyl dodecyl bromination ammonium (DMDA), 0.3 gram ethylene glycol diacrylate, 50mL solvent hexanaphthene and 1 Ke Siban-60 add in the reactor, be warming up to 75 ℃ under constantly stirring, drip the initiator ammonium persulfate copolyreaction after 4 hours, filter, the dry water-absorbing resin powder that gets of methanol wash is then with 100 parts of chloroprene rubbers, 30 parts of water-absorbing resin powders, 1 part of stearic acid, 5 parts of zinc oxide, 4 parts of magnesium oxide, 1 part of anti-aging agent, 30 parts of potter's clay carry out blend in mill, vulcanize can water-swellable in 25 ℃ to 150 ℃ scopes rubber.Take by weighing these hydro-expansive rubber 8 grams and deionized water 80 grams, put into autoclave, sealing is warming up to 150 ℃ of insulations after 3 days with autoclave, reduces to room temperature rapidly, takes out sample, wipes the moisture on surface with filter paper, and weighing gets 43 grams.
Embodiment 8
With 2.5 gram vinylformic acid, 3 gram sodium acrylates, 3.5 gram acrylamide, 1 gram vinylformic acid stearyl alcohol ester, 0.4 Diethylene Glycol double methacrylate, 50mL solvent hexanaphthene and 1 gram tween-80 add in the reactor, be warming up to 75 ℃ under constantly stirring, drip the initiator ammonium persulfate copolyreaction after 4 hours, filter, the dry water-absorbing resin powder that gets of methanol wash is then with 100 parts of ethylene-propylene rubber(EPR), 30 parts of water-absorbing resin powders, 5 parts of zinc oxide, 1 part of stearic acid, 2 parts of promotor, 1.5 part sulphur, 20 parts of carbon blacks carry out blend in mill, vulcanize can water-swellable in 25 ℃ to 150 ℃ scopes rubber.Take by weighing these hydro-expansive rubber 8 grams and deionized water 80 grams, put into autoclave, sealing is warming up to 150 ℃ of insulations after 3 days with autoclave, reduces to room temperature rapidly, takes out sample, wipes the moisture on surface with filter paper, and weighing gets 43 grams.

Claims (8)

1, a kind of method for preparing high-temperature-rusistance water-expansible rubber, it is characterized in that with mass ratio being vinylformic acid, sodium acrylate, acrylamide, heat resist modification monomer and the linking agent of 20-40: 30-60: 10-50: 10-60: 0.1-10, add in the reactor with solvent and dispersion agent, stir the back of heating up and drip the initiator copolyreaction, refilter, methanol wash dry the water-absorbing resin powder, the blend in mill with rubber and water-absorbing resin powder then, add vulcanizing ingredient vulcanize high-temperature-rusistance water-expansible rubber.
2, a kind of method for preparing high-temperature-rusistance water-expansible rubber according to claim 1 is characterized in that the heat resist modification monomer is a vinyl-acetic ester, butyl acrylate, Octyl acrylate, vinylformic acid lauryl alcohol ester, vinylformic acid stearyl alcohol ester, butyl methacrylate, Octyl methacrylate, methacrylic acid lauryl alcohol ester, methacrylic acid stearyl alcohol ester, 2-acrylamido-2-methyl propane sulfonic acid, 3-acrylamido oxypropyl trimethyl ammonium chloride, methacryloyl amido oxypropyl trimethyl ammonium chloride, dimethyl diallyl ammonium chloride or 2-methylacryoyloxyethyl-dimethyl dodecyl bromination ammonium.
3, a kind of method for preparing high-temperature-rusistance water-expansible rubber according to claim 1, it is characterized in that linking agent is ethylene glycol diacrylate, Diethylene Glycol double methacrylate, polyoxyethylene glycol double methacrylate, N, N '-methylene-bisacrylamide, tetramethylolmethane double methacrylate or Vinylstyrene.
4, a kind of method for preparing high-temperature-rusistance water-expansible rubber according to claim 1 is characterized in that solvent is toluene, dimethylbenzene and hexanaphthene.
5, a kind of method for preparing high-temperature-rusistance water-expansible rubber according to claim 1 is characterized in that dispersion agent is span-80, Si Ban-60, Si Ban-20, tween-80, Tween-60, tween 20, Sodium dodecylbenzene sulfonate.
6, a kind of method for preparing high-temperature-rusistance water-expansible rubber according to claim 1 is characterized in that rubber is natural rubber, chloroprene rubber, ethylene-propylene rubber(EPR), paracril, chlorinatedpolyethylene, urethanes, viton, silicon rubber, isoprene-isobutylene rubber or styrene-butadiene rubber(SBR).
7, the method for preparing hydro-expansive rubber according to claim 1, the granularity that it is characterized in that the water-absorbing resin powder is less than 5 μ m.
8, the method for preparing hydro-expansive rubber according to claim 1 is characterized in that initiator is Potassium Persulphate or ammonium persulphate.
CNB2005100199726A 2005-12-08 2005-12-08 Method for preparing high-temperature-rusistance water-expansible rubber Expired - Fee Related CN1331936C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2005100199726A CN1331936C (en) 2005-12-08 2005-12-08 Method for preparing high-temperature-rusistance water-expansible rubber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2005100199726A CN1331936C (en) 2005-12-08 2005-12-08 Method for preparing high-temperature-rusistance water-expansible rubber

Publications (2)

Publication Number Publication Date
CN1775849A true CN1775849A (en) 2006-05-24
CN1331936C CN1331936C (en) 2007-08-15

Family

ID=36765577

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2005100199726A Expired - Fee Related CN1331936C (en) 2005-12-08 2005-12-08 Method for preparing high-temperature-rusistance water-expansible rubber

Country Status (1)

Country Link
CN (1) CN1331936C (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101963051A (en) * 2010-02-08 2011-02-02 张宏亮 Oil well packer
CN101967240A (en) * 2010-09-21 2011-02-09 重庆市万通工业有限公司 Water swelling rubber, metallic composite sealing material and preparation methods thereof
CN101974193A (en) * 2010-11-17 2011-02-16 武汉工程大学 Method for preparing low-leaching-rate water-swellable rubbers
CN101407601B (en) * 2008-11-20 2011-07-20 武汉工程大学 Method for modifying water encounter swelling rubber by using hydrophobic monomer
CN103554333A (en) * 2013-11-19 2014-02-05 宜兴丹森科技有限公司 Preparation method of high strength super absorbent resin
CN103570985A (en) * 2013-10-09 2014-02-12 中国石油化工股份有限公司 Water-swelling rubber composite material, and preparation method and application thereof
CN106084347A (en) * 2016-06-23 2016-11-09 安徽荣达阀门有限公司 A kind of low temperature resistant water-swellable water proof rubber encapsulant and preparation method thereof
CN107641274A (en) * 2017-09-30 2018-01-30 咸阳橡胶工业制品研究所有限公司 Type high-temperature-rusistance water-expansible rubber composite seal and preparation method during one kind control
CN109354734A (en) * 2018-10-25 2019-02-19 西北橡胶塑料研究设计院有限公司 A kind of flame retardant type hydro-expansive rubber material and preparation method thereof
CN110527058A (en) * 2019-07-30 2019-12-03 浙江神州科技化工有限公司 A kind of water-swellable body material synthesis method

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07100786B2 (en) * 1986-05-30 1995-11-01 シ−アイ化成株式会社 Water-swellable waterproof composition
JP2592567B2 (en) * 1992-06-19 1997-03-19 シーアイ化成株式会社 Water swellable rubber
CZ70097A3 (en) * 1997-03-07 1998-09-16 Jiří Ing. Šulc Composite water-swelling elastomers and process for preparing thereof
DE19800489A1 (en) * 1998-01-09 1999-07-15 Thomas Prof Dr Mang Polysaccharide-containing sealing composition
JP4103108B2 (en) * 2002-06-11 2008-06-18 東洋ゴム工業株式会社 Rubber composition for tire tread

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101407601B (en) * 2008-11-20 2011-07-20 武汉工程大学 Method for modifying water encounter swelling rubber by using hydrophobic monomer
CN101963051A (en) * 2010-02-08 2011-02-02 张宏亮 Oil well packer
CN101967240A (en) * 2010-09-21 2011-02-09 重庆市万通工业有限公司 Water swelling rubber, metallic composite sealing material and preparation methods thereof
CN101974193A (en) * 2010-11-17 2011-02-16 武汉工程大学 Method for preparing low-leaching-rate water-swellable rubbers
CN101974193B (en) * 2010-11-17 2011-12-07 武汉工程大学 Method for preparing low-leaching-rate water-swellable rubbers
CN103570985A (en) * 2013-10-09 2014-02-12 中国石油化工股份有限公司 Water-swelling rubber composite material, and preparation method and application thereof
CN103554333A (en) * 2013-11-19 2014-02-05 宜兴丹森科技有限公司 Preparation method of high strength super absorbent resin
CN106084347A (en) * 2016-06-23 2016-11-09 安徽荣达阀门有限公司 A kind of low temperature resistant water-swellable water proof rubber encapsulant and preparation method thereof
CN107641274A (en) * 2017-09-30 2018-01-30 咸阳橡胶工业制品研究所有限公司 Type high-temperature-rusistance water-expansible rubber composite seal and preparation method during one kind control
CN109354734A (en) * 2018-10-25 2019-02-19 西北橡胶塑料研究设计院有限公司 A kind of flame retardant type hydro-expansive rubber material and preparation method thereof
CN110527058A (en) * 2019-07-30 2019-12-03 浙江神州科技化工有限公司 A kind of water-swellable body material synthesis method
CN110527058B (en) * 2019-07-30 2022-01-14 浙江神州科技化工有限公司 Method for synthesizing water-swellable material

Also Published As

Publication number Publication date
CN1331936C (en) 2007-08-15

Similar Documents

Publication Publication Date Title
CN1775849A (en) Method for preparing high-temperature-rusistance water-expansible rubber
CN106589225B (en) Polymer gel particles for deep profile control and water shutoff and preparation method thereof
CN109320673B (en) Self-repairing flexible hydrogel electro-sensitive material and preparation method and application thereof
CN101407601B (en) Method for modifying water encounter swelling rubber by using hydrophobic monomer
EP1309634B1 (en) Water-soluble or water-swellable, associatively thickening copolymers containing sulfo groups, method for producing the same and use thereof
CN110760152B (en) Anti-freezing hydrogel and preparation method and application thereof
CN107556423B (en) Preparation method of high-strength and high-toughness double-physical-crosslinking polyacrylic acid hydrogel
EP3161028B1 (en) Copolymer containing oxazoline monomers and use thereof as a cross-linking agent
DE102006050761A1 (en) Hydrophobically modified cationic copolymers
DE102006007004A1 (en) Water-soluble sulfo-containing copolymers, process for their preparation and their use
DE102007012786A1 (en) Preparation of sulfo-containing copolymers
Ren et al. Super-tough, ultra-stretchable and strongly compressive hydrogels with core–shell latex particles inducing efficient aggregation of hydrophobic chains
CN112322268A (en) Stretchable slow-expansion acrylic resin and preparation process and application thereof
CN115572347A (en) High-temperature-resistant high-salt-resistant tackifying and shearing-improving agent for water-based drilling fluid and preparation method and application thereof
WO2020135149A1 (en) Acrylamide copolymer and preparation method therefor and use thereof
CN108276716B (en) Graphene/acrylate rubber composite material and preparation method thereof
CN1244603C (en) High-performace water-absorbing expansion rubber and process for preparing same
CN110790859B (en) Acrylamide copolymer and preparation method and application thereof
EP1608602B1 (en) Use of a cross-linked polymer composition as a water-absorbing constituent in sealing and absorption materials
CN104609770A (en) Micro-spherical hydration heat regulating agent as well as preparation method and application of micro-spherical hydration heat regulating agent
CN112079591B (en) Method for synthesizing environment-responsive polymer by copolymerization modification of alkenyl sulfonate monomer
KR20080053686A (en) Method for preparing vinyl chloride graft copolymer resin
CN113332936A (en) High-toughness conductive anti-freezing carbon nanotube organic hydrogel
CN110790860B (en) Acrylamide copolymer and preparation method and application thereof
CN103265662B (en) A kind of preparation method of crosslinkable fluid loss agent

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20070815

Termination date: 20100108